Device for the treatment of polluted water

ABSTRACT

An apparatus for aerating polluted water is disclosed herein. The apparatus includes a tubular section defining a primary chamber having an opening in the side for admission of air from the surrounding atmosphere. A principle distribution chamber for receiving water to be aerated is connected to an upper peripheral edge of the tubular section and delivers water to a plurality of high speed nozzles that deliver accelerated sprays into the primary chamber. A tapering section is connected to a lower peripheral edge of the tubular section. A venturi section is connected to the lower peripheral edge of the tapering section. A single drain pipe including an upper peripheral edge is connected to a lower peripheral edge of the venturi and constitutes the sole outlet of the device. The nozzles create an air water mixture in the primary chamber and are directed toward the venturi to create a suction effect thereby drawing additional air into the primary chamber through the inlet orifice.

This application is a divisional of continuation application U.S. Ser.No. 08/320,567, filed Oct. 11, 1994, by Antonio Caballero, entitled"DEVICE AND METHOD FOR THE TREATMENT OF POLLUTED WATER", still pending,which is a continuation application of parent application U.S. Ser. No.08/010,144, filed Jan. 28, 1993, by Antonio Caballero Pichardo, entitled"DEVICE AND METHOD FOR THE TREATMENT OF POLLUTED WATER" now abandoned.

TECHNICAL FIELD

The present invention relates to water pollution control devices. Moreparticularly, the present invention relates to apparatus and methods forthe aeration of polluted water.

BACKGROUND ART

During the treatment of waste water or polluted water, it is oftennecessary to aerate the water. As used herein, the terms "waste water"and "polluted water" are used interchangeably. During the process ofaeration, a sufficient amount of oxygen is furnished to the water so asto allow the elimination of contaminants by multiplying aerobic bacteriain the water being treated. This plays an important part in thedegradation process of the organic wastes contained in the water.

The uncontrolled growth of the world's population has simultaneouslyproduced a problem of great magnitude. This problem is an insufficientsupply of water needed to satisfy the demand for water. The irrationaluse of water, and its pollution, has appreciably aggravated the supplyof water. The pollution of water through the lack of control ofcontaminated industrial waste has made obsolete the natural systemstraditionally used to assist in the decontamination of water, such asriver channels. Such river channels are no longer sufficient to degradethe organic material from sewage discharges.

In an attempt to solve this problem, the installation of industrialplants to treat the waste water has been promoted. However, thepercentages of organic and fecal matter have increased to the point thatthese plants, which were initially efficient, have now been overcome bythe problem and have been left idle because of poor results. As anexample, over half of the waste water treatment plants which wereinstalled in Mexico have fallen into disuse. The rest of such wastewater treatment plants have been operating with great deficiencies andinefficiencies.

There are various techniques that can be used for the introduction ofair into the water for the purpose of aerating the waste water. Forexample, mechanical waterfalls have been used to break up the water in afashion similar to the flow in rivers and streams. Unfortunately, thisaction is not sufficient because the channels in rivers and streamscontain abundant spaces and unevenness. These are conditions that cannotbe obtained in a treatment plant of this type. In the treatment plants,such spaces are reduced and the unevenness or drops are limited. In thismanner, the aeration of the water in these mechanical waterfalls hasbeen very low in comparison with that obtained in the channels of riversor streams.

Aeration tanks have been used for the purpose of treating pollutedwater. In aeration tanks, water passes through a tank with orifices. Theintent of this process is that the liquid absorbs the air enteringthrough these holes. Since this action is considered natural, notforced, the air does not penetrate the flow of water because the wateroffers resistance. Consequently, the results of this device discourageits use.

Another technique used for the treatment of polluted water is the use ofagitators and mechanical revolving devices. These can be subdivided intotwo types: (1) the surface agitator and (2) the submerged revolvingdevice. The surface water agitator is installed in a tank withpreviously calculated dimensions. The action of the agitator breaks upthe water so as to force it to take in air from the surface. Althoughthis action is efficient, it is limited to aerating the water locatedwithin a few centimeters of the surface. Unfortunately, it is unable toagitate the deeper water. Subsequently, there is no aeration and thetransference of oxygen to all of the water in the tank is notaccomplished. Consequently, although this device permits a goodassimilation of air to the surface water, it has the disadvantage ofproviding almost no aeration at the bottom of the tank. The surfacewater agitator also has the disadvantage of creating a "short circuit."When the surface water is sufficiently aerated, it promotes thereproduction of aerobic bacteria. However, on the bottom of the tank,the desired aeration is not found. As such, the reproduction ofanaerobic bacteria occurs. This causes the "short circuit" since theoxidizing enzymes from the aerobic bacteria kill the anaerobic bacteriaand vice versa.

The submerged revolving device is an apparatus which moves water fromthe deeper parts. Unfortunately, large amounts of electricity arerequired so as to break up the water. Without this large amount ofpower, the agitation is not performed in the required efficient mannerso as to obtain the necessary aeration. This device requires a highconsumption of electrical current so as to achieve a vigorous agitationof the water to be treated. The high power consumption of such a devicepresents a great disadvantage.

Air blowers have been used for the aeration of water. Various types ofair blowers have been employed in the past in an attempt to achieve theproper aeration of water. Air blowers are devices that can supply largeamounts of air at relatively low pressure. This presents a greatdisadvantage since water, an element which presents more resistance thanair, does not allow the air to penetrate easily. Consequently, theresults of water aeration through the use of air blowers has beendeficient.

Compressors and turbo compressors have been used in an effort to find anapparatus that could efficiently furnish air to water for the purposesof oxygenating polluted water. These devices introduce air at higherpressures. This equipment requires a high consumption of electricalenergy so as to achieve its purposes. From a cost-benefit analysis, theuse of compressors and turbo compressors cannot be justified for thetreatment of waste water or for the treatment of polluted water.

It is evident that all of the devices described hereinabove haveattempted to solve the problem by introducing air to water. This hasresulted in various complications. Because of the density differencebetween water and air, the water will present resistance to theintroduction of air. In order to reach this objective, an expensivepiece of equipment is required which can consume a large amount ofenergy. Additionally, whenever air is introduced in the water using highpressure, the air enters at high velocity and exits to the surface atpractically the same velocity. Under these conditions, little oxygen isyielded to the water. It is doubtful that the results justify theinvestment.

It is an object of the present invention to provide a device and methodfor the treatment of contaminated water which is both efficient andeconomical.

It is another object of the present invention to provide a method andapparatus for the treatment of water which maximizes the surface areaavailable for contact between the oxygen and the air.

It is a further object of the present invention to provide a method andapparatus for the treatment of polluted water which relies on naturalreactions between water and air.

It is still a further object of the present invention to provide anapparatus and method for the treatment of waste water which is morecost-effective than conventional equipment.

It is still a further object of the present invention to provide a wastewater treatment device which is easily adaptable to the variousconditions which apply at the site.

These and other objects and advantages of the present invention willbecome apparent from a reading of the attached specification andappended claims.

SUMMARY OF THE INVENTION

The present invention is a device for the treatment of polluted waterthat comprises a primary chamber, a principal distribution chamberhaving an inlet connected to a source of polluted water, a secondarydistribution chamber connected to a supply of polluted water, an airinlet orifice formed in the primary chamber so as to allow air to passinto the primary chamber, a venturi connected in fluid communicationwith the primary chamber, and a drain pipe connected to the venturi forallowing an air/water mixture to flow from the outlet of the venturi.The principal distribution chamber has a plurality of spray nozzlesconnected thereto and positioned into the primary chamber. The spraynozzles serve to pass polluted water into the primary chamber. Thesecondary distribution chamber has a plurality of high-speed nozzlespositioned within the primary chamber. These high-speed nozzles serve topass the polluted water into the primary chamber. The venturi ispositioned below the primary chamber. The venturi serves to acceleratethe flow of the air/water mixture passing from the primary chamber.

The principal distribution chamber is a circular body which extendsaround the circumference of the primary chamber. The principaldistribution chamber has a plurality of spray nozzles which arepositioned into the primary chamber. The secondary distribution chamberis positioned within the primary chamber. The secondary distributionchamber has an inlet extending through the primary chamber to the supplyof polluted water. The principal distribution chamber and the secondarydistribution chamber are arranged independently of each other within theprimary chamber. The source of polluted water for both the principaldistribution chamber and the secondary distribution chamber are thesame. The high-speed nozzles of the secondary distribution chamber aredirected downwardly toward the venturi. The venturi has a wide portionconnected to the primary chamber. The venturi narrows in diameter fromthe wide portion toward the drainpipe.

The principal distribution chamber has an inspection door which isremovably connected thereto. The inspection door allows physical accessto the interior of the principal distribution chamber. Similarly, thesecondary distribution chamber has a second inspection door removablyconnected thereto. The secondary inspection door enables physical accessto the secondary distribution chamber. In a like manner, the primarychamber has an inspection door which is removably connected thereto.This inspection door allows physical access to the interior of theprimary chamber.

The air inlet orifice has a protective screen extending thereover. Theair inlet orifice is positioned along the top of the primary chamber.The protective screen has a size and configuration suitable for impedingthe passage of foreign matter therethrough.

The present invention is also a method of treating polluted water whichcomprises the steps of: (1) passing a flow of polluted water throughspray nozzles into a primary chamber; (2) introducing another flow ofpolluted water through a high-speed nozzle into the primary chamber; (3)drawing air into the primary chamber; (4) accelerating a flow ofpolluted water and air through a venturi so as to mix the polluted waterwith the air; and (5) drawing the mixed air/water from an outlet of theventuri.

The step of passing a flow includes the steps of distributing the flowof polluted water around a circumference of the primary chamber andspraying the polluted water through the spray nozzles into the primarychamber. The step of passing another flow includes the steps ofaccumulating the polluted water in a secondary distribution chamberwithin the primary chamber and spraying the polluted water downwardlythrough the high-speed nozzles toward the venturi. The spray nozzlesassociated with the primary distribution chamber pass a greater volumeof polluted water than the high-speed nozzles associated with thesecondary distribution chamber. The flows of polluted water come fromthe same source. The step of drawing occurs simultaneously with the stepof accelerating. The step of drawing includes the step of cavitating theair/water mixture so as to maximize a volume of air relative to thevolume of water.

In general, the present invention is a cylindrical body furnished with apair of inlets for the entrance of the water to be treated. The firstinlet distributes the water into the primary distribution chamber wherethe pressure is homogenized. Then the water is distributed to a seriesof spray nozzles so as to allow the polluted water to be distributed inthe form of a mist or spray. These nozzles are strategically andgeometrically placed around the primary distribution chamber. The secondinlet introduces the water into the secondary distribution chamber wherethe pressure is homogenized and the water is distributed to variousnozzles. These nozzles are of the "filled cone" type. These nozzlesserve to accelerate the water so as to project it at high speed to theventuri. The venturi produces an acceleration of the water which, uponexiting the narrow portion of the venturi, creates a suction effectwhich drags with it the air/water mixture formed inside the primarychamber. At the same time, the air in the mixture is drawn through anorifice located in the upper section of the primary chamber.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a side view of the aerator device in accordance with thepreferred embodiment of the present invention.

FIG. 2 is a cross-sectional side view of the present invention.

FIG. 3 is a side cutaway view of the secondary distribution chamber ofthe present invention.

FIG. 4 is a top view of the plate where the nozzles of the secondarydistribution chamber are positioned.

FIG. 5 is a cross-sectional side view of the nozzles of the secondarydistribution chamber.

FIG. 6 is a cross-sectional side view of the venturi in accordance withthe present invention.

FIG. 7 is a bottom view showing the venturi in accordance with thepresent invention.

FIG. 8 shows an alternative embodiment of the aeration device of thepresent invention.

FIG. 9 is a cross-sectional side view of the alternative embodiment ofthe present invention as shown in FIG. 8.

FIG. 10 is a side view of another alternative embodiment of the aerationdevice of the present invention.

FIG. 11 is a cutaway view of the alternative embodiment of the presentinvention as illustrated in FIG. 10.

FIG. 12 is a side view of still another alternative of the presentinvention.

FIG. 13 is a cross-sectional view of the alternative embodiment of thepresent invention as shown in FIG. 12.

DETAILED DESCRIPTION OF THE INVENTION

The aeration device 100 is comprised of a generally cylindrical bodyhaving a primary chamber 10. The primary chamber 10 is connected to asecond section 15 which contains a narrow portion tapering to the lowerend of the device. This lower end of the device is a venturi system 40.The venturi system 40 is described hereinbelow. The aeration device, asshown in FIG. 1, has a primary inlet 20 located at the top, for waterbeing treated. The device 100 also has a second inlet 30, also for waterbeing treated, placed essentially at the center of the device 100.

Both of the inlets 20 and 30 are connected to a common supply line forwater to be treated (not shown). This line accommodates the flow to bothinlets. Inlet 20 is connected to a principal distribution chamber 25 ofcircular dimension. The principal distribution chamber 25 is equippedwith several spray nozzles 27. The water enters the primary chamber 10through the nozzles 27. The water is broken up and projected in anatomized condition into the primary chamber 10 of the device 100. Inlet30 is connected to a secondary distribution chamber 35. Secondarydistribution chamber 35 is equipped with a system of high-speed nozzles37. These nozzles 37 provide high velocity to the water as it exits thenozzles and enters the venturi system 40 of the device 10.

The water is distributed through the supply pipe to the chambers 25 and35 where the pressure of the liquid is homogenized. The primarydistribution chamber 25 receives approximately seventy-five percent ofthe flow. The primary distribution chamber 25 distributes the wateramong the spray nozzles 27 installed therein. These nozzles break up thewater in such a way that it enters the primary chamber 10 in a mistform. The quantity of nozzles is determined by the volume and pressureof water to be treated. This arrangement obtains a homogeneods andfinely-divided mixture so as to enhance the oxygenation of the water.

The secondary distribution chamber 35 receives the balance of the flow,approximately twenty-five percent. The secondary distribution chamber 35is positioned centrally of the primary chamber 10. The secondary chamber35 passes the water through the nozzles 37 installed therein. Thenozzles 37 are of the cone type. These cone-type nozzles cause the waterto pass through the tapered hole of each nozzle. The tapered hole ofeach nozzle causes the water to acquire a high velocity and,subsequently, projects the water to the lower part of the primarychamber 10 and toward the venturi system 40.

When the water is projected into the venturi system 40, it leaves thenozzles 37, exiting at high speed, and acquires a higher acceleration onits path toward the outlet. The outlet is the narrowest part of thedevice 100. The high-velocity water outlet produces a reaction of thesame magnitude and in the opposite direction. This reaction is thesuction of the air/water mixture which has been accumulated in theprimary chamber 10 of the device 100. The water takes the air/watermixture along with it as it exits through the drainpipe 50. This samesuction resupplies the primary chamber 10 of the device 100 with the airthat enters through the orifice 60. The orifice 60 is equipped with aprotective screen 65 so as to prevent the entrance of foreign particlesthat could affect the operation of the aeration device 100 of thepresent invention.

For the purposes of inspecting the interior of the aeration device 100,the device 100 is furnished with inspection doors 70 and 75 at the levelof the primary distribution chamber 25 and the secondary distributionchamber 35, respectively. These inspection doors 70 and 75 can beremoved or opened so that physical access to the interior of thechambers 25 and 35 can be obtained. These inspection doors can also beused so as to observe the conditions of cleanliness. It is important tobe able to inspect the interior of the device 100 so as to prevent theobstruction and to maintain the general operation of the nozzles 27 andthe nozzles 3,4. The secondary distribution chamber 35 contains aninspection door so as to provide access to the nozzles. Each of theseinspection doors is attached using conventional methods which facilitatetheir removal and replacement (e.g., bolts, nuts, washers, packing,etc.).

With respect to the venturi system 40, the venturi system is a generallyconical section whose narrow portion is calculated such that it causesan acceleration of the water which passes inside. Once the water flowpasses through the narrowest section, it expands again and falls throughthe pipe 50 into a sump placed at a preselected distance. Thispreselected distance will vary with the altitude above sea level atwhich the device is installed.

As mentioned previously, the narrowing of the cone of the venturi system40 produces an acceleration of the water. This acceleration is inaddition to the acceleration caused by gravity acting on the water. Theacceleration is of such a magnitude that a reaction in the oppositedirection occurs so as to create a suction which drags the air/watermixture, previously accumulated in the primary chamber 10 of the device100. Cavitation also occurs between the air and the water as it passesthrough the venturi.

The arrangement of the invention which has been described above andwhich is shown in FIGS. 1-7 provides the most efficient aeration thatcan be achieved. This aeration is accomplished through the use of threeseparate processes of water aeration. The first aeration is achievedwhen the water passes through the series of nozzles 27. When the waterpasses through nozzles 27, the water becomes atomized, sprayed, or inmist form. The second aeration occurs to the flow of water by theeffects of the suction created when the water is accelerated by passingthrough the narrow portion of the venturi cone. Through the suctionprocess, the flowing water drags air out of the mixture formed in theprimary chamber 10. According to tests carried out on the mixture of airand water contained in the main chamber, compositions of 24 and up to 30parts of air per part of water were reported. These compositionsoccurred at favorable conditions at sea level. The third aeration isproduced when the water falls into a sump, with a previously calculateddepth. This aeration occurs because, as the air attempts to free itselffrom the water in which it is trapped, the mixture falls through thedrainpipe from a height of approximately 7.2 meters (23.6 feet). When itis freed, the air produces a large quantity of bubbles. The water willthen have a high probability of absorbing all of the oxygen that willdissolve within the water.

Although the above arrangement is the most efficient, such anarrangement is not always necessary. For example, for less flow volumeor less contaminated water, it will not be necessary to use thisembodiment. Consequently, three other more economical arrangements arepresented herein for water flows of lesser volume.

FIGS. 8 through 13 correspond to three variations of the presentinvention. The technical characteristics of these variations of thecontaminated water aeration device of the present invention aregenerally equivalent to those described under the preferred embodiment,as described in FIGS. 1-7.

The variation illustrated in FIGS. 8 and 9 differs from the first inthat, in the second embodiment, the mixture does not include a primarydistribution chamber 25, nor the spray nozzles 27. Also, secondarydistribution chamber 35 and the high velocity nozzles 37 are located inthe top part of the device such that the orifice or opening 60 for theair inlet is placed at the side of the main section of the primarychamber. For this embodiment, a large number of high velocity nozzlesare provided so as to produce a large pull of air due to the narrowingof the cone section. This must occur because water is not being sprayedor atomized as in the manner described in conjunction with the preferredembodiment of the present invention.

In another variation of the present invention, as represented by FIGS.10 and 11, the primary distribution chamber 25 and the spray nozzles 27are also omitted. The remainder of the elements, such as the secondarydistribution chamber 35 and the high-velocity nozzles 34 as well as theorifice or opening 60 for the entrance of air, and the screen 75, retainthe same arrangement as that shown in the preferred embodiment of thepresent invention.

The fourth embodiment of the present invention, as shown in FIGS. 12 and13, presents, at the top, a special chamber 80 for the entrance of waterto be treated. This chamber may be equipped with a single nozzle at thecenter, and also with three, four, or up to five high-velocity nozzles37. Orifice 60, for the entrance of air, is placed at one side of themain chamber of the device.

This embodiment of the invention is appropriate for small or mediumflows. For example, with a single nozzle, between one and three litersper second can be handled. With three nozzles, between three to nineliters per second can be handled. With four nozzles, between four totwelve liters per second can be handled. With five nozzles, between fiveto fifteen liters per second can be handled.

The three alternative embodiments of the present invention operate bythe same principles of the preferred embodiment. The common elementsbetween the alternative embodiments of the present invention and thepreferred embodiment of the present invention, such as the nozzlechamber (as shown in FIG. 3), the venturi section 40, and the orifice60, each have basically the same structure as that described andillustrated in the preferred embodiment.

The foregoing disclosure and description of the invention isillustrative and explanatory thereof. Various changes in the details ofthe illustrated construction or in the steps of the described method canbe made within the scope of the appended claims without departing fromthe true spirit of the invention. The present invention should only belimited by the following claims and their legal equivalents.

I claim:
 1. An aeration device, comprising:a tubular section defining aprimary chamber, said tubular section having an opening in a sidethereof forming an orifice adjacent said primary chamber for theadmission of ambient air from the surrounding atmosphere into saidprimary chamber, said tubular section having an upper peripheral edgeand a lower peripheral edge; a screen for preventing the entrance offoreign particles positioned over the orifice in said tubular section;means defining a distribution chamber for receiving a liquid to beaerated; said distribution chamber positioned above and sealinglyconnected to the upper peripheral edge of said tubular section; aplurality of high speed nozzels positioned at a top end of said primarychamber and fluidly connected to said distribution chamber fordelivering accelerated sprays of liquid from said distribution chamberto said primary chamber; a tapering section having an upper peripheraledge and a lower peripheral edge, wherein the upper peripheral edge ofsaid tapering section is positioned below and sealingly connected to thelower peripheral edge of said tubular section, and wherein a diameter ofthe upper peripheral edge of said tapering section is larger than adiameter of the lower peripheral edge of said tapering section; aventuri section including an upper peripheral edge and a lowerperipheral edge, wherein the upper peripheral edge of said venturisection is positioned below and sealingly connected to the lowerperipheral edge of the tapering section for accelerating the air andliquid therefrom with the entrapped air and for creating a suction atthe orifice for drawing air into said primary chamber; a single drainpipe having an upper peripheral edge that is sealingly connected to thelower peripheral edge of said venturi section, said drain pipe having alower open end, wherein said drain pipe constitutes the sole outlet ofsaid device such that all of the liquid and air entering said deviceexits said device through said drain pipe wherein said tapering section,said venturi section, and said drain pipe each have respective maximumcross sectional areas that are substantially smaller than a maximumcross sectional flow area of said primary chamber.
 2. An aeration devicein accordance with claim 1, wherein said distribution chamber includesan inspection door to provide access to the interior thereof.